US10017617B2ActiveUtilityA1
Peroxide treated metallocene-based polyolefins with improved melt strength
Assignee: CHEVRON PHILLIPS CHEMICAL CO LPPriority: May 14, 2013Filed: Jul 7, 2017Granted: Jul 10, 2018
Est. expiryMay 14, 2033(~6.8 yrs left)· nominal 20-yr term from priority
C08F 10/02B29C 48/022B29C 48/10B29C 39/003C08F 8/00B29C 48/397B29K 2023/0658C08F 210/16C08K 5/14B29K 2023/08C08F 2810/10B29L 2007/008B29K 2105/0094B29K 2105/0085C08J 2323/04C08J 2323/08C08J 2323/26B29K 2995/0088C08J 2323/06B29C 48/0018B29K 2023/0625B29C 48/08C08J 5/18B29C 47/40B29C 49/0005B29C 47/0004B29C 47/0057B29C 47/0026B29C 47/385B29C 47/0021C08L 23/0815C08L 23/04C08F 210/02B29C 48/40
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References
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Claims
Abstract
Disclosed herein are ethylene-based polymers having low densities and narrow molecular weight distributions, but high melt strengths for blown film processing. Such polymers can be produced by peroxide-treating a metallocene-catalyzed resin.
Claims
exact text as granted — not AI-modifiedThe invention claimed is:
1. A method of making a film comprising an ethylene polymer, the method comprising:
(i) providing an ethylene polymer having a ratio of Mw/Mn of less than or equal to about 5, a ratio of Mz/Mw of less than or equal to about 2.3, and a zero-shear viscosity at 190° C. of greater than or equal to about 1×10 5 Pa-sec;
wherein the ethylene polymer is further characterized by a peak melting point in a range from about 100 to about 120° C., a vicat softening temperature in a range from about 95 to about 110° C., and a difference between the peak melting point and the vicat softening temperature of less than or equal to about 16° C.; and
(ii) melt processing the ethylene polymer through a film die to form the film.
2. The method of claim 1 , wherein:
the method comprises melt processing the ethylene polymer and at least one additive through the die; and
the ethylene polymer is an ethylene/α-olefin copolymer.
3. The method of claim 2 , wherein the film is a blown film.
4. The method of claim 3 , wherein the ethylene/α-olefin copolymer is produced by a process comprising melt processing a mixture of a base resin and a peroxide compound in a twin screw extrusion system at a temperature in a range from about 120 to about 300° C. to generate peroxide groups at about 10-50 ppm of peroxide groups based on the weight of the base resin.
5. The method of claim 1 , wherein the ethylene polymer is further characterized by:
a melt index in a range from about 0.05 to about 2;
a ratio of HLMI/MI in a range from about 15 to about 50; and
a density in a range from about 0.895 to about 0.928 g/cm 3 .
6. The method of claim 1 , wherein:
the ratio of Mw/Mn is in a range from about 2 to about 5; and
the ratio of Mz/Mw is in a range from about 1.5 to about 2.3.
7. The method of claim 6 , wherein the zero-shear viscosity at 190° C. is in a range from about 1×10 5 to about 2×10 6 Pa-sec.
8. The method of claim 7 , wherein the film is a blown film or a cast film, and is characterized by a thickness in a range from about 0.5 to about 250 mils.
9. The blown film or cast film prepared by the method of claim 8 .
10. A method of making a film comprising an ethylene/α-olefin copolymer, the method comprising:
(i) providing an ethylene/α-olefin copolymer having:
a ratio of Mw/Mn in a range from about 2 to about 4;
a ratio of Mz/Mw in a range from about 1.5 to about 2.2;
a melt index in a range from 0 to about 1;
a zero-shear viscosity at 190° C. of greater than or equal to about 1×10 5 Pa-sec;
a density in a range from about 0.91 to about 0.92 g/cm 3 ; and
from about 0.008 to about 0.04 long chain branches (LCB) per 1000 total carbon atoms; and
(ii) melt processing the ethylene/α-olefin copolymer through a film die to form the film.
11. The method of claim 10 , wherein the copolymer is further characterized by:
a peak melting point in a range from about 105 to about 120° C.; and
a vicat softening temperature in a range from about 95 to about 110° C.
12. The method of claim 10 , wherein the copolymer is further characterized by a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28.
13. The method of claim 10 , wherein:
the ethylene/α-olefin copolymer is produced by a process comprising melt processing a mixture of a base resin and a peroxide compound at a weight ratio of peroxide groups of the peroxide compound in a range from about 10 to about 60 ppm, based on the weight of the base resin; and
step (ii) comprises melt processing the ethylene/α-olefin copolymer and at least one additive through the film die to form the film.
14. The method of claim 10 , wherein the film is a blown film or a cast film, and is characterized by a thickness in a range from about 0.5 to about 250 mils.
15. The blown film or cast film prepared by the method of claim 14 .
16. A method of making a film comprising an ethylene/1-hexene copolymer, the method comprising:
(i) providing an ethylene/1-hexene copolymer having:
a ratio of Mw/Mn of less than or equal to about 5;
a ratio of Mz/Mw of less than or equal to about 2.3;
a zero-shear viscosity at 190° C. of greater than or equal to about 1×10 5 Pa-sec;
a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28; and
a density in a range from about 0.905 to about 0.925 g/cm 3 ; and
(ii) melt processing the ethylene/1-hexene copolymer through a film die to form the film.
17. The method of claim 16 , wherein:
the ratio of Mw/Mn is in a range from about 2 to about 3.5; and
the ratio of Mz/Mw is in a range from about 1.5 to about 2.2.
18. The method of claim 17 , wherein:
the CY-a parameter at 190° C. is in a range from about 0.08 to about 0.18; or
the zero-shear viscosity at 190° C. is in a range from about 1×10 5 to about 2×10 6 Pa-sec; or
both.
19. The method of claim 17 , wherein the film is a blown film or a cast film, and is characterized by a thickness in a range from about 0.5 to about 250 mils.
20. The blown film or cast film prepared by the method of claim 19 .
21. A method of making a film comprising an ethylene/α-olefin copolymer, the method comprising:
(i) providing an ethylene/α-olefin copolymer having a ratio of Mw/Mn of less than or equal to about 5, a ratio of Mz/Mw of less than or equal to about 2.3, and a zero-shear viscosity at 190° C. of greater than or equal to about 1×10 5 Pa-sec;
wherein the ethylene/α-olefin copolymer is further characterized by a CY-a parameter at 190° C. in a range from about 0.08 to about 0.28, or from about 0.008 to about 0.04 long chain branches (LCB) per 1000 total carbon atoms, or both, and a density in a range from about 0.895 to about 0.928 g/cm 3 , and
(ii) melt processing the ethylene/α-olefin copolymer through a film die to form the film.
22. The method of claim 21 , wherein:
the ratio of Mw/Mn is in a range from about 2 to about 5;
the ratio of Mz/Mw is in a range from about 1.5 to about 2.3; and
the zero-shear viscosity at 190° C. is in a range from about 1×10 5 to about 2×10 6 Pa-sec.
23. The method of claim 22 , wherein the ethylene/α-olefin copolymer is further characterized by:
a melt index in a range from about 0.05 to about 2; and
a ratio of HLMI/MI in a range from about 15 to about 50.
24. The method of claim 22 , wherein the film is a blown film or a cast film, and is characterized by a thickness in a range from about 0.5 to about 250 mils.
25. The blown film or cast film prepared by the method of claim 24 .Join the waitlist — get patent alerts
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